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US4368114A Expired / Lapsed US ⏱️ 0.0 years remaining

Octane and total yield improvement in catalytic cracking

Assignee: Mobil Oil AS
•
Filing: 1981-09-14
•
Granted: 1983-01-11
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Expires: 2001-09-14
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Abstract

Abstract Octane and total yield improvement in catalytic cracking processes can be attained by the addition to conventional cracking catalysts of very small amounts of additive catalyst comprising a class of zeolites characterized by a silica to alumina mole ratio greater than about 12 and a constraint index of about 1 to 12. The additive catalyst is added to the conventional cracking catalyst in the cracking process in an amount which provides the zeolite component of the additive catalyst at from about 0.01 weight percent to about 1.0 weight percent of the conventional cracking catalyst in the cracking process.

Inventors

  • 👤 Arthur W. Chester
  • 👤 William E. Cormier, Jr.
  • 👤 William A. Stover

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 19:51
CPC Classifications
B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/80; B01J29/40; B01J37/00; B01J37/04; C; C10; C10G; C10G11/00; C10G11/02; C10G11/04; C10G11/05; B01J2229/00; B01J2229/10; B01J2229/26; B01J2229/30; B01J2229/36; B01J2229/42; B01J29/08; B01J29/084; B01J29/65; B01J29/70

Claims Analysis

Total Claims: 17
Claim 1
Independent Claim 109 words
In a process for catalytic cracking of petroleum fractions in the presence of a conventional cracking catalyst comprising at least about 5 weight percent of a catalytically active component and under cracking conditions, the improvement wherein separate additive catalyst comprising a zeolite characterized by a Constraint Index of from about 1 to about 12 and a silica to alumina mole ratio greater than about 12 is added to said conventional cracking catalyst in the cracking process in an amount which provides the zeolite component of said separate additive catalyst at from about 0.01 weight percent to about 1.0 weight percent of the conventional cracking catalyst in the cracking process.
Claim 2
Dependent Claim 109 words
In a process for catalytic cracking of petroleum fractions in the presence of a conventional cracking catalyst comprising at least about 5 weight percent of a catalytically active component and under cracking conditions, the improvement wherein separate additive catalyst comprising a zeolite characterized by a Constraint Index of from about 1 to about 12 and a silica to alumina mole ratio greater than about 12 is added to said conventional cracking catalyst in the cracking process in an amount which provides the zeolite component of said separate additive catalyst at from about 0.01 weight percent to about 1.0 weight percent of the conventional cracking catalyst in the cracking process.
Claim 3
Dependent Claim 45 words
The process of claim 1 wherein said separate additive catalyst is added in an amount which provides the zeolite component of said separate additive catalyst at from about 0.05 weight percent to about 0.5 weight percent of the conventional cracking catalyst in the cracking process.
Claim 4
Dependent Claim 31 words
The process of claim 1 wherein said zeolite of the separate additive catalyst is at least one member selected from the group consisting of ZSM-5, ZSM-11, ZSM-12, ZSM-23, ZSM-35 and ZSM-38.
Claim 5
Dependent Claim 10 words
The process of claim 3 wherein said zeolite is ZSM-5.
Claim 6
Dependent Claim 35 words
The process of claim 1 wherein said catalytically active component of the conventional cracking catalyst is at least one member selected from the group consisting of amorphous silica alumina, crystalline silica alumina and crystalline zeolite.
Claim 7
Dependent Claim 29 words
The process of claim 5 wherein said crystalline zeolite of said conventional cracking catalyst is selected from the group consisting of zeolite X, zeolite Y and naturally occurring faujasite.
Claim 8
Dependent Claim 17 words
The process of claim 6 wherein said crystalline zeolite of said conventional cracking catalyst is zeolite Y.
Claim 9
Dependent Claim 17 words
The process of claim 4 wherein said crystalline zeolite of said conventional cracking catalyst is zeolite Y.
Claim 10
Dependent Claim 17 words
The process of claim 1 wherein the catalytic cracking takes place in a fluid catalytic cracking process.
Claim 11
Dependent Claim 22 words
The process of claim 1 wherein the addition of said separate additive catalyst occurs during an on-stream operation of the cracking process.
Claim 12
Dependent Claim 53 words
The process of claim 1 wherein a metal selected from the group consisting of platinum, palladium, iridium, osmium, rhodium, ruthenium and rhenium is added to the conventional cracking catalyst in an amount of from about 0.01 ppm to about 100 ppm, based on total catalyst inventory, in order to enhance carbon monoxide conversion.
Claim 13
Dependent Claim 54 words
The process of claim 1 wherein a metal selected from the group consisting of platinum, palladium, iridium, osmium, rhodium, ruthenium and rhenium is added to the separate additive catalyst in an amount of from about 1.0 ppm to about 1000 ppm, based on total separate additive catalyst, in order to enhance carbon monoxide conversion.
Claim 14
Dependent Claim 13 words
The process of claim 1 wherein the separate additive catalyst is intermittently added.
Claim 15
Dependent Claim 38 words
The process of claim 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12 or 13 wherein said zeolite of the separate additive catalyst has a silica to alumina mole ratio of between 12 and infinity.
Claim 16
Dependent Claim 18 words
The process of claim 1 wherein the improvement includes increased yield of C 5 + gasoline and alkylate.
Claim 17
Dependent Claim 17 words
The process of claim 1 wherein the improvement includes a cracking process product of increased octane number.

References Cited (Backward Citations)

US3686121A Cited
US3758403A Cited
US3748251A Cited
US3847793A Cited
US4239654A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-01-10 1986-07-12 1987-01-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-01-10 1990-07-12 1991-01-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-01-10 1994-07-12 1995-01-11 $7700.00 Window Closed / Lapsed

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